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 Dortmund Data Bank
Thermophysical Data for Process Design
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Query
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DDB# Name CAS-RN Formula
161 Toluene 108-88-3 C7H8 Overview Details
174 Water 7732-18-5 H2O Overview Details
1050 Carbon dioxide 124-38-9 CO2 Overview Details
1065 Hydrogen sulfide 7783-06-4 H2S Overview Details
2187 Methyldiethanolamine (MDEA) 105-59-9 C5H13NO2 Overview Details
Search for mixtures containing this mixture as subsystem
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Mixture Data

Databank Sets Points Temperature
Range		 Pressure
Range
Vapor-Liquid Equilibria VLE 39 354 289-606 K6-35000 kPa
161 174 1050
1
174 1050 1065
10
174 1050 1065 2187
1
174 1050 2187
22
174 1065 2187
5
Gas Solubilities GLE 381 2898 283-473 K0-1,8302E7 kPa
174 1050 2187
323
174 1065 2187
58
Liquid-Liquid Equilibria (Miscibility Gaps) LLE 21 149 270-453 K335-30000 kPa
161 174 1050
1
161 174 2187
16
174 1050 1065
4
Heat Capacities of Mixtures, Excess Heat Capacities CPE 4 39 298 K (const.)n.a.
174 1050 2187
4
Densities and Volumes of Mixtures, Excess Volumes VE 16 108 298-423 K101-808 kPa
174 1050 2187
16
Mixture Viscosities VIS 44 390 293-394 K6-13946 kPa
161 1050 1065
10
174 1050 1065 2187
3
174 1050 2187
25
174 1065 2187
6
Mixture Surface Tensions MSFT 14 203 298-350 K110-15600 kPa
174 1050 1065
1
174 1050 1065 2187
3
174 1050 2187
8
174 1065 2187
2
Mixture P-v-T Data MPVT 33 617 293-423 K5-14921 kPa
161 1050 1065
9
174 1050 1065 2187
2
174 1050 2187
18
174 1065 2187
4
Gas Hydrate Data GHD 7 24 263-288 K316-10310 kPa
174 1050 1065
7
Diffusion Coefficients DIF 8 71 288-323 Kn.a.
174 1050 2187
6
174 1065 2187
2
Further Thermodynamic Properties X 290 11395 278-422 K2-19950 kPa
161 174 1050 1065 2187
10
161 174 1050 2187
5
161 174 1065 2187
4
161 174 2187
5
161 1050 1065
16
174 1050 1065
1
174 1050 1065 2187
21
174 1050 2187
187
174 1065 2187
41
Total 857 16248
161 174 1050
2
161 174 1050 1065 2187
10
161 174 1050 2187
5
161 174 1065 2187
4
161 174 2187
21
161 1050 1065
35
174 1050 1065
23
174 1050 1065 2187
30
174 1050 2187
609
174 1065 2187
118

Dortmund Data Bank Version: February 2024
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